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Effect of Index on Curing Kinetics & Viscoelastic Properties of PU gels

Lifeng Wu

TRFA 2006 Annual Meeting

September 11, 2006

HUNTSMAN POLYURETHANES

Polyurethanes

Gel: a colloidal system consisting of a liquid which is dispersed in a solid polymeric matrix resulting in a soft, gelly, material.

Applications: Adhesives Energy absorbers, dampers

Gel

Polyurethanes

PU Gels

Hydrogel Poly(ethylene oxide) network swelled with water

Plasticizer gel PU network plasticized with phthalates

Polyol gel: PU network with excess multifunctional polyol

Monol gel*: Polyol mixture of diol and monol crosslinked with

multifunctional isocyanates

* US6908979 and US6914117 (Huntsman patents)

Polyurethanes

Polyol Gel

Materials: Rubinate 1209: prepolymer based on MDI (NCO% = 21.5) Jeffol G31-55: polyether triol (OHv = 55)

Jeffcat TD-33A: tertiary amine catalyst

OH

HO

HO

+NCOOCN

OH

NCO

H

O

OCNH

OCat.

Index: r [NCO]0/[OH]0

r = 0.5 – 1.0

Conversion: p ([NCO]0 – [NCO])/[NCO]0

Polyurethanes

Rheology

Rheology: study of the flow and deformation of matter.

AR 2000 Rheometer

G’: storage modulus

G”: loss modulus

: phase angle = tan-1(G”/G’)

G”

G’

liquid solid

Polyurethanes

Curing Rheology (r = 0.5, 0.6)

r = 0.5

1.0E-01

1.0E+01

1.0E+03

1.0E+05

1.0E+07

0 20 40 60 80 100

t (min)

G',

G"

(Pa

)

0

30

60

90

(

de

g)

G'

G"

r = 0.6

1.0E-01

1.0E+01

1.0E+03

1.0E+05

1.0E+07

0 20 40 60 80 100

t (min)

G',

G"

(Pa

)

0

30

60

90

(

de

g)

G'

G"

Gel Point: G’ = G”

Polyurethanes

Curing Rheology (r = 0.7, 0.8)

r = 0.7

1.0E-01

1.0E+01

1.0E+03

1.0E+05

1.0E+07

0 20 40 60 80 100

t (min)

G',

G"

(Pa

)

0

30

60

90

(

de

g)

G'

G"

r = 0.8

1.0E-01

1.0E+01

1.0E+03

1.0E+05

1.0E+07

0 20 40 60 80 100

t (min)

G',

G"

(Pa

)

0

30

60

90

(

de

g)

G'

G"

Similar behavior to r = 0.6.

Polyurethanes

Curing Rheology (r = 0.9, 1.0)

r = 0.9

1.0E-01

1.0E+01

1.0E+03

1.0E+05

1.0E+07

0 20 40 60 80 100

t (min)

G',

G"

(Pa

)

0

30

60

90

(

de

g)

G'

G"

r = 1.0

1.0E-01

1.0E+01

1.0E+03

1.0E+05

1.0E+07

0 20 40 60 80 100

t (min)

G',

G"

(Pa

)

0

30

60

90

(

de

g)

G'

G"

G” shows 2nd stage growth . High crosslink density

Polyurethanes

Curing kinetics

0

1

2

3

4

0 2 4 6 8 10 12 14

(1-r)t

Ln

[(1

-rp

)/(1

-p)]

k[H]0 = 0.28 min-1k[NCO][OH]

t

[NCO]

d

d

r)t(1k[OH])p-1

rp-1ln( 0

re

1et)p(r, r)t(1k[H]

r)t(1k[H]

0

0

Molecular weight*: Mw(r,p)

Crosslink density*: (r,p)

* Macosko and Miller, 1976

Gel Point

Polyurethanes

Viscosity at Initial Stage

1.0E-01

1.0E+00

1.0E+01

1.0E+02

1.0E+03

1.0E+04

0 2 4 6 8 10

t (min)

G"

(Pa

)

1.0E-01

1.0E+00

1.0E+01

1.0E+02

1.0E+03

1.0E+04

G' (

Pa

)

r = 0.5r = 0.6r = 0.7r = 0.8r = 0.9r = 1.0r = 1.0

Viscosity 0 = G”/ ( = 1 rad/s)

Polyurethanes

Initial Growth of Molecular Weight

1000

10000

100000

0 1 2 3 4 5 6

t (min)

Mw

(g

/mo

l)

1

10

100

1000

10000

G"

(Pa

)

r = 0.5r = 0.6r = 0.7r = 0.8r = 0.9r = 1.0r = 1.0

0 ~ Mw for unentangled polymers 0 ~ Mw

3.4 for entangled polymers

0 ~ Mw2

Entanglement

Polyurethanes

Crosslink Density –

0

0.2

0.4

0.6

0.8

1

0 20 40 60 80 100t (min)

r = 0.6 r = 0.7 r = 0.8

r = 0.9 r = 1.0

320 )

rp

1(2[OH]μ

0

0.2

0.4

0.6

0.8

1

0 20 40 60 80 100t (min)

1.0E+00

1.0E+01

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

G"

(Pa)

r = 0.6 r = 0.7 r = 0.8

r = 0.9 r = 1.0 r = 0.9

r = 1.0

G"

Polyurethanes

Viscoelastic Properties (r = 0.5,0.6)

r = 0.5

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

0.01 1 100 10000aT (rad/s)

G',

G"

(Pa

)

G'

G"

r = 0.6

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

0.01 1 100 10000aT (rad/s)

G',

G"

(Pa

)

G'

G"

G’ ≈ G” ~ 0.5 (critical gel) G’ ~ 0 (low ),G” ~ 0.5

Polyurethanes

Viscoelastic Properties (r = 0.7,0.8)

r = 0.7

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

0.01 1 100 10000aT (rad/s)

G',

G"

(Pa

)

G'

G"

r = 0.8

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

0.01 1 100 10000aT (rad/s)

G',

G"

(Pa

)

G'

G"

G’ ~ 0, G” ~ 0.5

Polyurethanes

Viscoelastic Properties (r = 0.9,1.0)

r = 0.9

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

0.01 1 100 10000aT (rad/s)

G',

G"

(Pa

)

70 °C

30 °C

50 °C

G'

G"

r = 1.0

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

0.01 1 100 10000aT (rad/s)

G',

G"

(Pa

) 30 °C

50 °C

70 °C

G'

G"

r = 0.9

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

0.01 1 100 10000aT (rad/s)

G',

G"

(Pa

)

70 °C

30 °C

50 °C

G'

G"

r = 1.0

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

0.01 1 100 10000aT (rad/s)

G',

G"

(Pa

) 30 °C

50 °C

70 °C

G'

G"

G’ ~ 0, G” ~ 0 – 0.5

Polyurethanes

Plateau Modulus – G0

1.E+03

1.E+04

1.E+05

1.E+06

1.E+07

0.5 0.6 0.7 0.8 0.9 1

r

G0 (

Pa

)

1.E+03

1.E+04

1.E+05

1.E+06

1.E+07

0.5 0.6 0.7 0.8 0.9 1

r

G0 (

Pa

)

μRT2

1G0

Polyurethanes

Curing Rheology at High Indices

1.0E-01

1.0E+00

1.0E+01

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

1.0E+07

0 20 40 60 80 100t (min)

G',

G"

(Pa

)

0

0.2

0.4

0.6

0.8

1

1.2

(

mo

l/L)

G'

G"

r = 1.0

Polyurethanes

r = 1.0

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

1.0E+07

0.01 0.1 1 10 100 1000 10000aT (rad/s)

G',

G"

(Pa

)

30 min_G'

30 min_G"

G'

G"

Relaxation Behavior During Curing

r = 1.0

1.0E+02

1.0E+03

1.0E+04

1.0E+05

1.0E+06

1.0E+07

0.01 0.1 1 10 100 1000 10000aT (rad/s)

G',

G"

(Pa

)

30 min_G'

30 min_G"

90 min_G'

90 min_G"

G'

G"

G” ~ 0.5G” ~ 0

Polyurethanes

Mechanism: Dangling Chains

NCO

H

O

OCNH

O

NCO

H

O

OH

NCO

H

O

OCNH

O

G” ~ 0.5

G” ~ 0

Before transition:

After transition:

< 0.4 mol/L dangling chains > 50%

> 0.6 mol/L dangling chains < 25%

Polyurethanes

Conclusion

Before gel point: Initial and Mw growth is nearly independent of index:

log() ~ t

After gel point: index r crosslink density #dangling chain

G’(), G”() : r = 0.5: G’ ≈ G” ~ 0.5 (critical gel) r = 0.6 – 0.8: G’ ~ 0, G” ~ 0.5 r = 0.9, 1.0: G’ ~ 0, G” ~ 0 – 0.5 (2nd stage growth)

Polyurethanes

Effect of Conversion on Mw and

Macosko and Miller, 1976

Mw

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